Cavern battery bank

ABSTRACT

A battery bank for a redox flow battery having a cavity in which electrolyte is stored, wherein the electrolyte is provided for supply to one or more redox flow cells, wherein the cavity is a cavern.

FIELD

The present invention relates to a battery bank for a redox flowbattery, to a redox flow battery having such a battery bank and to amethod for producing a battery bank for a redox flow battery. Theinvention further relates to the use of a cavern, in particular a saltdome cavern, as a battery bank.

BACKGROUND

A redox flow battery, also known as a flow battery, is anelectrochemical energy storage system. A redox flow battery isconventionally made up of a galvanic cell and two separate electrolytecircuits. The galvanic cell is divided into two half-cells by amembrane. Each half-cell is supplied by a separate electrolyte circuit,wherein the respective electrolyte is stored in tanks and pumped to therespective half-cell.

An anolyte is passed through a first half-cell and a catholyte throughthe second half-cell. An exchange of charge occurs between theelectrolytes. During charging and discharging, the anolyte and catholyteare respectively reduced and oxidized to convert electrical energy intochemical energy and vice versa.

Such a redox flow battery is known for example from document DE 10 2012016 317 A1.

The storage capacity of a redox flow battery is limited by the storagecapacity of the tanks for storing the electrolytes. In known systems, aplurality of tank containers are interconnected to store electrolyte.Further containers serve to accommodate a membrane system which servesas a galvanic cell for input and output of energy. As the capacity of aredox flow battery increases in such systems, the number of containersrequired for storing the electrolytes therefore rises and thus so toodoes the complexity of the plant engineering.

SUMMARY

The object of the present invention is accordingly to provide a batterybank for a redox flow battery, a redox flow battery having such abattery bank and a method for producing a battery bank for a redox flowbattery which do not exhibit the above-described disadvantages or atleast exhibit them to a reduced extent and in particular simply andinexpensively provide a redox flow battery with a high storage capacity.A further object is to state a use for a cavern.

The above-described object is achieved by a battery bank for a redoxflow battery, and the following description discloses advantageousdevelopments of the invention.

Accommodating the electrolyte in a cavern means that even large volumesof electrolyte can be stored in a single storage location or singlecavity. Caverns previously provided as gas caverns may, for example, beused for this purpose. No above-ground containers or tanks for storingelectrolyte are therefore required. As a consequence, plant costs andcomplexity for storing electrolyte for large capacity redox flowbatteries can be reduced, since there is no need for a widely branchedpipework system for linking a plurality of tanks or containers together.

When a cavern is mentioned in the present document, it is taken to be anunderground cavity which may for example be located several hundredmeters below the earth's surface.

The electrolyte which is accommodated in the battery bank is for examplea catholyte or an anolyte for a redox flow battery.

The electrolyte may have, for example, a storage capacity or energydensity of 25 watt-hours per liter (W*h/l).

A further development of the battery bank provides that the cavern is asalt dome cavern. Such a salt dome cavern may have been produced inknown manner by flushing or solution mining an underground salt stratum.Known methods can accordingly be used to create an underground cavitywhich serves as a battery bank for storing electrolyte for a redox flowbattery. It is alternatively possible to use a pre-existing cavern,which was originally provided for gas storage, for storing electrolytefor a redox flow battery.

Alternative developments may provide that the cavern is bounded at leastin places, in particular completely, by rocks, in particular granite.

A further development of the battery bank provides that the electrolytecomprises brine and polymer, in particular liquid polymer. In comparisonwith acid-based electrolytes, such an electrolyte has the advantage ofgreater environmental compatibility.

By using brine and polymer as electrolyte, it is possible to ensure thatfor example existing salt dome caverns, which were originally providedfor storing gas, can be repurposed as a battery bank for a redox flowbattery without additional environmental impact. Accordingly, a gascavern which has already been flooded with brine can for example beconnected to a circuit of a redox flow battery, wherein the brine can becombined with polymer during circulation. The brine can be enriched withpolymer by above-ground addition of polymer to the brine. In thismanner, large storage capacities can be utilized at comparatively lowcost as battery banks for a redox flow battery.

When brine is mentioned in the present document, it is taken to mean asaturated aqueous saline solution.

A further development of the battery bank provides that the cavity has avolume (cavity volume) in an inclusive range from 70,000 m³ (seventythousand cubic meters) to 500,000 m³ (five hundred thousand cubicmeters) or 500,000 m³ (five hundred thousand cubic meters) to 800,000 m³(eight hundred thousand cubic meters), in particular 600,000 m³.

These volumes are of the orders of magnitude in which for example saltdome caverns for gas storage are conventionally produced. Large volumesof electrolyte can accordingly be stored in a single battery bank withlow plant costs. For example, a cavern with a volume of approx. 600,000m³ (six hundred thousand cubic meters) can serve as a battery bank forstoring electrolyte.

New salt dome caverns can be created as battery banks for a redox flowbattery or existing gas storage salt dome caverns can be repurposed asbattery banks for a redox flow battery. It goes without saying that, inaddition to salt dome caverns, other types of caverns, such as forexample granite caverns or the like, can be suitable for storingelectrolyte for a redox flow battery.

Depending on the nature of the strata, it can be provided that thevolume of a cavern which is to serve as a battery bank for a redox flowbattery amounts to 100,000 m³ (one hundred thousand cubic meters) to1,000,000 million m³ (one million cubic meters). Insofar as permitted bygeological and technical constraints, the volume or the cavity volume ofa cavern which is to serve as a battery bank for a redox flow battery isfreely scalable, and can also hold in excess of one million cubic metersof electrolyte.

A further aspect of the invention relates to a redox flow battery havingone or more redox flow cells and at least two battery banks forsupplying one or more redox flow cells with electrolyte. At least one ofthe battery banks takes the form provided by the invention.

While the electrolyte, for example a catholyte, of at least one circuitof such a redox flow battery is stored underground in a cavern, theelectrolyte, for example an anolyte, of a second circuit of the redoxflow battery can be conventionally stored above ground in containers ortanks. Underground storage of even at least one electrolyte of a redoxflow battery reduces the space required above ground and the plantengineering for interlinked above-ground tanks or containers.

When a redox flow cell is mentioned in the present document, it is takento mean a galvanic cell which is divided into at least two half-cells byone or more membranes. An anolyte is passed through a first half-celland a catholyte through the second half-cell. An exchange of chargeoccurs between the electrolytes. During charging and discharging, theanolyte and catholyte are respectively reduced and oxidized to convertelectrical energy into chemical energy and vice versa.

A further development of the redox flow battery provides providing twoor more battery banks for supplying the one or more redox flow cellswith electrolyte, wherein at least two battery banks take the formprovided by the invention. According to this development, at least twobattery banks for storing electrolyte are arranged underground incaverns. In this manner, large storage volumes and capacities can beprovided for a redox flow battery while keeping plant costs low. Forexample, a first battery bank according to the invention can store ananolyte and a second battery bank, separate from the first battery bank,can store a catholyte.

An alternative development of a redox flow battery provides that theredox flow battery is provided with precisely two battery banks forsupplying the one or more redox flow cells with electrolyte, wherein thebattery banks are constructed in the manner according to the invention.This development makes it straightforwardly possible to provide a redoxflow battery which has a high storage volume or capacity, wherein plantengineering can be minimized because there are only two battery banks orelectrolyte stores. For example, a plurality of redox flow cells can befed and supplied with electrolyte from precisely two separate,underground caverns, wherein the first battery bank stores an anolyteand the second battery bank, separate from the first battery bank,stores a catholyte.

While the battery banks can be provided at least in part, preferablyexclusively, underground in caverns, the one or more redox flow cells,which are also designated membrane stacks, are preferably arranged aboveground.

A further development of the redox flow battery provides that a firstpipe string and a second pipe string for supplying and withdrawingelectrolyte open into the cavern, wherein the pipe strings are inparticular nested in one another. Existing pipe strings, for exampleremaining from a previous use of the cavern for gas storage, canaccordingly be reused or modified for supplying and/or withdrawingelectrolyte.

To save space, the pipe strings can be nested in one another. Forexample, the first pipe string can be suspended in a second pipe string.

With regard to the plant engineering for a redox flow battery which mayhave a widely branched metallic pipework system, it is advantageous touse brine with polymer as the electrolyte since the metal pipes are notattacked by the brine.

When it is stated in the present document that the first and the secondpipe strings open into the cavern, this means that at least one end ofthe respective pipe string extends into the cavity volume of the cavernwhich is provided for storing electrolyte.

A further development of the redox flow battery provides that one end ofthe first pipe string is associated with a cavern floor and one end ofthe second pipe string is associated with a cavern roof.

When the battery is in operation, stratification can arise in theelectrolyte during battery charging or discharging. For example, duringdischarging, charged electrolyte may be arranged or concentrated in theregion of the cavern roof above discharged electrolyte, while dischargedelectrolyte collects in the region of the cavern floor. Duringdischarge, charged electrolyte can therefore be withdrawn via the secondpipe string from the roof area of the cavern and discharged electrolytecan be returned to the cavern via the second pipe string in the regionof the cavern floor.

The power output and power uptake capabilities of a redox flow celldepend on the one hand on the energy density and volume of theelectrolyte and furthermore on the available membrane area within theredox flow cells via which charge exchange can proceed. Flexibleadjustment of power uptake and power output of the redox flow batterycan be achieved by providing a plurality of redox flow cells, whereinthe redox flow cells can be arranged in a cascade system. The cascadesystem means the redox flow cells can be linked in in parallel or inseries with one another or excluded from the energy flow in line withrequirements in order to take account of current operating conditionswith regard to energy storage or power output.

The redox flow battery can have a capacity in a range from 12.5 to 25gigawatt hours (GWh) inclusive. Storage capacities which range up to thecapacity of a nuclear power station can thus be achieved with theproposed redox flow battery.

The redox flow battery can serve as buffer storage for wind or solarenergy power plants. It is advantageous here that a redox flow batterydoes not suffer any memory effect and is not damaged by deep discharge.

A further aspect of the invention relates to a method for producing abattery bank for a redox flow battery, wherein at least the followingmethod steps are carried out:

-   -   provision of a cavity for storing electrolyte, wherein the        cavity is a cavern;    -   provision of electrolyte in the cavern.

In the “provision of a cavity for storing electrolyte, wherein thecavity is a cavern” method step use may for example be made ofpre-existing caverns which were originally provided for gas storage.Alternatively, a new cavern for storing electrolyte can be created usingknown methods, wherein for example a salt dome can be solution mined.The brine may here remain in the cavern and be combined with polymer.

Electrolyte can be introduced into the cavern after or during solutionmining of the cavern. For example, salt dome caverns already floodedwith brine can be gradually combined with polymer, in particular liquidpolymer, in a circulating brine circuit in order to provide theelectrolyte required for a redox flow battery.

Alternatively, a gas cavern can be directly filled or flooded with anelectrolyte composed of brine and polymer and so be used as a batterybank for a redox flow battery.

A final aspect of the invention relates to the use of a cavern, inparticular a salt dome cavern, as a battery bank for accommodatingelectrolyte for a redox flow battery. The cavern may in particular herebe a salt dome cavern which was originally provided or used for gasstorage.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention is described in greater detail below on the basis ofdrawings which diagrammatically illustrate exemplary embodiments, inwhich:

FIG. 1 shows a redox flow battery according to the invention with abattery bank according to the invention.

FIG. 2 shows a battery bank according to the invention for a redox flowbattery.

DETAILED DESCRIPTION

FIG. 1 shows a redox flow battery 2. The redox flow battery 2 has afirst battery bank 4 and a second battery bank 6. The first battery bank4 has a cavity 8 in which electrolyte 10 is stored. The cavity 8 is acavern 8.

The second battery bank 6 has a cavity 12 in which electrolyte 14 isstored. The cavity 12 is a cavern 12.

The electrolyte 10 comprises brine and liquid polymer. The electrolyte14 likewise comprises brine and liquid polymer. In the present case,electrolyte 10 forms the anolyte. Electrolyte 14 forms the catholyte.

The cavern 8 has a cavity volume for accommodating electrolyte 10 of600,000 m³. The cavern 12 has a cavity volume for accommodatingelectrolyte 14 of 600,000 m³.

The redox flow battery 2 has a redox flow cell 16. The redox flow cell16 is subdivided by a membrane 18 into a first half-cell 20 and a secondhalf-cell 22. A first electrode 24 is associated with the firsthalf-cell 20. A second electrode 26 is associated with the secondhalf-cell 22. Electrical energy can be withdrawn from and supplied tothe redox flow cell 16 via the electrodes 24, 26.

The first half-cell 20 is connected via pipework 28 to the first batterybank 4. The second half-cell 22 is connected via pipework 30 to thesecond battery bank 6. The electrolyte 10 is conveyed through the firsthalf-cell 20 with the assistance of a pump 31. The electrolyte 12 isconveyed through the second half-cell 22 with the assistance of a pump32. Two separate electrolyte circuits are formed in this manner.

The redox flow battery 2 may have a plurality of redox flow cells 16which are interconnected in a cascade system. The present redox flowbattery 2 has a capacity of 15 gigawatt hours (GWh).

FIG. 2 shows a battery bank 34 which can serve as a battery bank 4 or 6of the redox flow battery 2 shown in FIG. 1 . Battery bank 34accommodates electrolyte 36. Electrolyte 36 can be withdrawn from orsupplied to the battery bank 34 via a conveying system 38.

In the present case, the battery bank 34 has a salt dome cavern 35,which has been introduced into a salt dome 40 by solution mining, and acavity 35 for accommodating electrolyte 36.

The conveying system 38 comprises a riser 42, an anchor pipe string 44,a lining pipe string 46, a protective run 48, an electrolyte withdrawalrun 50 and an electrolyte return run 52.

The electrolyte return run 52 is a first pipe string 52 which opens intothe salt dome cavern 35. A first end 51 of the first pipe string 52 ishere associated with a cavern floor 54.

The electrolyte withdrawal run 50 is a second pipe string 50 which opensinto the salt dome cavern 35. A first end 53 of the second pipe string50 is here associated with a cavern roof 56.

During discharge of a redox flow battery, which can for example bedesigned as a redox flow battery 2 according to FIG. 1 , chargedelectrolyte 36 is withdrawn from the region of the cavern roof 56 viathe second pipe string 50 and supplied to one or more redox flow cells.

Discharged electrolyte 36 can be returned via the first pipe string 52to the cavern floor 54 of the salt dome cavern 35, once the chemicalenergy of the electrolyte 36 has been converted into electrical energyin one or more redox flow cells. This thus gives rise to stratificationwithin the salt dome cavern 35, wherein charged electrolyte 36 isassociated with or concentrated at the cavern roof 56 and dischargedelectrolyte 36 is associated with or concentrated at the cavern floor54.

The pumps 31, 32 can be operated in two directions, such that theelectrolyte circuits can also be operated in two directions. In thiscase, the second pipe string 50 is an electrolyte return run and thefirst pipe string 52 the electrolyte withdrawal run. The pumps 31, 32can be arranged within or outside the cavities 8, 10.

In the present case, a salt dome cavern 35 is therefore used as abattery bank 34, by an electrolyte 36, which is provided for supply to aredox flow battery, being stored in the salt dome cavern 35.

The battery bank 34 can on the one hand be produced by repurposing apre-existing gas cavern, which has been created in a salt dome bysolution mining, into a battery bank for storing electrolyte. Thebattery bank 34 may for example be an already flooded, brine-filled gascavern. Polymer can then gradually be supplied to the brine in a cycleprocess in order to provide an electrolyte for a redox flow battery inthe cavern.

Alternatively, a cavern can be incorporated into a salt domespecifically for use as a battery bank for a redox flow battery.

REFERENCE SIGNS

-   2 Redox flow battery-   4 First battery bank-   6 Second battery bank-   8 Cavity/cavern-   10 Electrolyte/anolyte-   12 Cavity/cavern-   14 Electrolyte/catholyte-   16 Redox flow cell-   18 Membrane-   20 First half-cell-   22 Second half-cell-   24 First electrode-   26 Second electrode-   28 Pipework-   30 Pipework-   31 Pump-   32 Pump-   34 Battery bank-   35 Salt dome cavern/cavity-   36 Electrolyte-   38 Conveying system-   40 Salt dome-   42 Riser-   44 Anchor pipe string-   46 Lining pipe string-   48 Protective run-   50 Electrolyte withdrawal run/second pipe string-   51 First end of the first pipe string-   52 Electrolyte return run/first pipe string-   53 First end of the second pipe string-   54 Cavern floor-   56 Cavern roof

What is claimed is:
 1. A battery bank for a redox flow battery,comprising: a cavity in which electrolyte is stored, wherein theelectrolyte is provided for supply to one or more redox flow cells,wherein the cavity is a salt dome cavern.
 2. The battery bank as claimedin claim 1, wherein the electrolyte comprises brine and polymer.
 3. Thebattery bank as claimed in claim 1, wherein the cavity has a volume inan inclusive range from 70,000 m³ to 500,000 m³, or 500,000 m³ to800,000 m³.
 4. A redox flow battery comprising: one or more redox flowcells; and at least two battery banks for supplying the one or moreredox flow cells with electrolyte, wherein at least one of the at leasttwo battery banks comprises a cavity in which the electrolyte is stored,wherein the cavity is a salt dome cavern.
 5. The redox flow battery asclaimed in claim 4, wherein at least two of the at least two batterybanks each comprises a cavity in which a respective electrolyte isstored, wherein each cavity is a salt dome cavern.
 6. The redox flowbattery as claimed in claim 4, wherein a first pipe string and a secondpipe string for supplying and withdrawing electrolyte open into the saltdome cavern, wherein the first and the second pipe strings are nested inone another, wherein one end of the first pipe string is associated witha cavern floor of the salt dome cavern and one end of the second pipestring is associated with a cavern roof of the salt dome cavern.
 7. Theredox flow battery as claimed in claim 4, wherein a plurality of redoxflow cells are provided, wherein the redox flow cells are arranged in acascade system, and/or the redox flow battery has a capacity in aninclusive range from 12.5 to 25 gigawatt hours (GWh).
 8. A method forproducing at least one battery bank for a redox flow battery,comprising: disposing a first electrolyte in a first cavity for storingelectrolyte, wherein the first cavity is a first salt dome cavern. 9.Use of a cavern as a battery bank for accommodating electrolyte for aredox flow battery, wherein the cavern is a salt dome cavern.
 10. Thebattery bank as claimed in claim 2, wherein the polymer is a liquidpolymer.
 11. The redox flow battery as claimed in claim 4, wherein theat least two battery banks for supplying the one or more redox flowcells with electrolyte consists of two battery banks for supplying theone or more redox flow cells with electrolyte, wherein the two batterybanks each comprise a cavity in which a respective electrolyte isstored, wherein each cavity is a salt dome cavern.
 12. The battery bankas claimed in claim 1, wherein the cavity has a volume in an inclusiverange from 100,000 m³ to 1,000,000 m³.
 13. The battery as claimed inclaim 4, wherein the cavity has a volume in an inclusive range from100,000 m³ to 1,000,000 m³.
 14. The battery as claimed in claim 4,wherein the electrolyte comprises brine and polymer.
 15. The method asclaimed in claim 8, wherein the first cavity has a volume in aninclusive range from 100,000 m³ to 1,000,000 m³.
 16. The method asclaimed in claim 8, wherein the first electrolyte comprises brine andpolymer.
 17. The method as claimed in claim 8, further comprising:disposing a second electrolyte in a second cavity for storingelectrolyte, wherein the second cavity is a second salt dome cavern. 18.The method as claimed in claim 17, wherein the second cavity has avolume in an inclusive range from 100,000 m³ to 1,000,000 m³ and/or thesecond electrolyte comprises brine and polymer.
 19. The use of a cavernas claimed in claim 9, wherein the cavern has a volume in an inclusiverange from 100,000 m³ to 1,000,000 m³.
 20. The use of a cavern asclaimed in claim 9, wherein the electrolyte comprises brine and polymer.